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  • C01B39/00—Compounds having molecular sieve and base-exchange properties, e.g. crystalline zeolites; Their preparation; After-treatment, e.g. ion-exchange or dealumination
  • C01B39/02—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof; Direct preparation thereof; Preparation thereof starting from a reaction mixture containing a crystalline zeolite of another type, or from preformed reactants; After-treatment thereof
  • C01B39/46—Other types characterised by their X-ray diffraction pattern and their defined composition
  • C01B39/48—Other types characterised by their X-ray diffraction pattern and their defined composition using at least one organic template directing agent
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  • B01J29/00—Catalysts comprising molecular sieves
  • B01J29/04—Catalysts comprising molecular sieves having base-exchange properties, e.g. crystalline zeolites
  • B01J29/06—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof
  • B01J29/70—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof of types characterised by their specific structure not provided for in groups B01J29/08 - B01J29/65
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  • C01B39/00—Compounds having molecular sieve and base-exchange properties, e.g. crystalline zeolites; Their preparation; After-treatment, e.g. ion-exchange or dealumination
  • C01B39/02—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof; Direct preparation thereof; Preparation thereof starting from a reaction mixture containing a crystalline zeolite of another type, or from preformed reactants; After-treatment thereof
  • C01B39/026—After-treatment
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
  • B01D—SEPARATION
  • B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
  • B01D53/34—Chemical or biological purification of waste gases
  • B01D53/74—General processes for purification of waste gases; Apparatus or devices specially adapted therefor
  • B01D53/86—Catalytic processes
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  • B01D53/8625—Nitrogen oxides
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  • B01D—SEPARATION
  • B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
  • B01D53/34—Chemical or biological purification of waste gases
  • B01D53/92—Chemical or biological purification of waste gases of engine exhaust gases
  • B01D53/94—Chemical or biological purification of waste gases of engine exhaust gases by catalytic processes
  • B01D53/9404—Removing only nitrogen compounds
  • B01D53/9409—Nitrogen oxides
  • B01D53/9413—Processes characterised by a specific catalyst
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  • B01J29/00—Catalysts comprising molecular sieves
  • B01J29/04—Catalysts comprising molecular sieves having base-exchange properties, e.g. crystalline zeolites
  • B01J29/06—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof
  • B01J29/70—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof of types characterised by their specific structure not provided for in groups B01J29/08 - B01J29/65
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  • B01J29/00—Catalysts comprising molecular sieves
  • B01J29/04—Catalysts comprising molecular sieves having base-exchange properties, e.g. crystalline zeolites
  • B01J29/06—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof
  • B01J29/70—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof of types characterised by their specific structure not provided for in groups B01J29/08 - B01J29/65
  • B01J29/72—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof of types characterised by their specific structure not provided for in groups B01J29/08 - B01J29/65 containing iron group metals, noble metals or copper
  • B01J29/74—Noble metals
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  • B01J29/00—Catalysts comprising molecular sieves
  • B01J29/04—Catalysts comprising molecular sieves having base-exchange properties, e.g. crystalline zeolites
  • B01J29/06—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof
  • B01J29/70—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof of types characterised by their specific structure not provided for in groups B01J29/08 - B01J29/65
  • B01J29/72—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof of types characterised by their specific structure not provided for in groups B01J29/08 - B01J29/65 containing iron group metals, noble metals or copper
  • B01J29/76—Iron group metals or copper
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
  • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
  • B01J29/00—Catalysts comprising molecular sieves
  • B01J29/04—Catalysts comprising molecular sieves having base-exchange properties, e.g. crystalline zeolites
  • B01J29/06—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof
  • B01J29/70—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof of types characterised by their specific structure not provided for in groups B01J29/08 - B01J29/65
  • B01J29/78—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof of types characterised by their specific structure not provided for in groups B01J29/08 - B01J29/65 containing arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
• • C—CHEMISTRY; METALLURGY
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  • C01P—INDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
  • C01P2002/00—Crystal-structural characteristics
  • C01P2002/70—Crystal-structural characteristics defined by measured X-ray, neutron or electron diffraction data
  • C01P2002/72—Crystal-structural characteristics defined by measured X-ray, neutron or electron diffraction data by d-values or two theta-values, e.g. as X-ray diagram
• • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
  • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
  • Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
  • Y02P30/00—Technologies relating to oil refining and petrochemical industry
  • Y02P30/20—Technologies relating to oil refining and petrochemical industry using bio-feedstock
• • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
  • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
  • Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
  • Y02P30/00—Technologies relating to oil refining and petrochemical industry
  • Y02P30/40—Ethylene production

Definitions

• This disclosure relates to a novel synthetic crystalline molecular sieve designated SSZ-108, its synthesis, and its use in sorption and catalytic processes.
• Molecular sieve materials both natural and synthetic, have been demonstrated in the past to be useful as adsorbents and to have catalytic properties for various types of organic conversion reactions.
• Certain molecular sieves such as zeolites, aluminophosphates, and mesoporous materials, are ordered, porous crystalline materials having a definite crystalline structure as determined by X-ray diffraction.
• Within the crystalline molecular sieve material there are a large number of cavities which may be interconnected by a number of channels or pores. These cavities and pores are uniform in size within a specific molecular sieve material.
• these materials Because the dimensions of these pores are such as to accept for adsorption molecules of certain dimensions while rejecting those of larger dimensions, these materials have come to be known as "molecular sieves" and are utilized in a variety of industrial processes.
• SSZ-108 a new molecular sieve, designated SSZ-108 and having a unique X-ray diffraction pattern, has now been synthesized using one or more of 1-butyl-l-methylpyrrolidinium cations and 1-butyl-l- methylpiperidinium cations as a structure directing agent.
• a molecular sieve having, in its as- synthesized form, an X-ray diffraction pattern including the peaks listed in Table 2.
• the molecular sieve In its as-synthesized and anhydrous form, the molecular sieve has a chemical composition comprising the following molar relationship:
• Q comprises one or more of 1-butyl-l-methylpyrrolidinium cations and 1- butyl-l-methylpiperidinium cations; and M is a Group 1 or Group 2 metal.
• a molecular sieve having, in its calcined form, an X-ray diffraction pattern including the peaks listed in Table 3.
• the molecular sieve In its calcined form, the molecular sieve has a chemical composition comprising the following molar relationship:
• n has a value of from 5 to 25.
• a method of synthesizing the molecular sieve described herein comprising (a) preparing a reaction mixture comprising: (1) a source of silicon oxide; (2) a source of aluminum oxide; (3) a source of a Group 1 or Group 2 metal; (4) a structure directing agent comprising one or more of 1-butyl-l-methylpyrrolidinium cations and 1-butyl-l-methylpiperidinium cations; (5) hydroxide ions; and (6) water; and (b) subjecting the reaction mixture to crystallization conditions sufficient to form crystals of the molecular sieve.
• an organic compound conversion process comprising contacting an organic compound under organic compound conversion conditions with a catalyst comprising an active form of the molecular sieve described herein.
• a process of selectively reducing nitrogen oxides (NO x ) comprising contacting a gas stream containing nitrogen oxides, with a catalyst comprising the molecular sieve described herein.
• FIG. 1 shows the powder X-ray diffraction (XRD) pattern of the as- synthesized molecular sieve of Example 1.
• FIG. 2 is a Scanning Electron Micrograph (SEM) image of the as- synthesized molecular sieve of Example 1.
• FIG. 3 shows the powder XRD pattern of the calcined molecular sieve of Example 6.
• the term "as-synthesized” is employed herein to refer to a molecular sieve in its form after crystallization, prior to removal of the structure directing agent.
• anhydrous is employed herein to refer to a molecular sieve substantially devoid of both physically adsorbed and chemically adsorbed water.
• the present molecular sieve is synthesized by: (a) preparing a reaction mixture comprising (1) a source of silicon oxide; (2) a source of aluminum oxide; (3) a source of a Group 1 or Group 2 metal (M); (4) a structure directing agent (Q) comprising one or more of 1-butyl-l-methylpyrrolidinium cations and 1-butyl-l- methylpiperidinium cations; (5) hydroxide ions; and (6) water; and (b) subjecting the reaction mixture to crystallization conditions sufficient to form crystals of the molecular sieve.
• a reaction mixture comprising (1) a source of silicon oxide; (2) a source of aluminum oxide; (3) a source of a Group 1 or Group 2 metal (M); (4) a structure directing agent (Q) comprising one or more of 1-butyl-l-methylpyrrolidinium cations and 1-butyl-l- methylpiperidinium cations; (5) hydroxide ions; and (6) water; and (b
• Suitable sources of silicon oxide silicon oxide include colloidal silica, fumed silica, precipitated silica, alkali metal silicates and tetraalkyi orthosilicates.
• Suitable sources of aluminum oxide include hydrated alumina and water-soluble aluminum salts (e.g., aluminum nitrate).
• Combined sources of silicon oxide and aluminum oxide can additionally or alternatively be used and can include aluminosilicate zeolites (e.g., zeolite Y) and clays or treated clays (e.g., metakaolin).
• zeolites e.g., zeolite Y
• clays or treated clays e.g., metakaolin
• the structure directing agent (Q) comprises one or more of 1-butyl-l- methylpyrrolidinium cations and 1-butyl-l-methylpiperidinium cations, represented by the following structures (1) and (2), respectively:
• Suitable sources of Q are the hydroxides, chlorides, bromides, and/or other salts of the quaternary ammonium compounds.
• Examples of suitable Group 1 or Group 2 metals (M) include sodium, potassium and calcium, with sodium being preferred.
• the metal is generally present in the reaction mixture as the hydroxide.
• the reaction mixture may contain seeds of a molecular sieve material, such as SSZ-108 crystals from a previous synthesis, in an amount of from 0.01 to 10,000 ppm by weight (e.g., 100 to 5000 ppm by weight) of the reaction mixture.
• the molecular sieve reaction mixture can be supplied by more than one source. Also, two or more reaction components can be provided by one source.
• reaction mixture can be prepared either batch wise or
• Crystal size, morphology and crystallization time of the molecular sieve described herein can vary with the nature of the reaction mixture and the
• Crystallization of the molecular sieve from the above reaction mixture can be carried out under either static, tumbled or stirred conditions in a suitable reactor vessel, such as for example polypropylene jars or Teflon-lined or stainless steel autoclaves, at a temperature of from 120°C to 200°C for a time sufficient for crystallization to occur at the temperature used, e.g., from 1 to 15 days.
• a suitable reactor vessel such as for example polypropylene jars or Teflon-lined or stainless steel autoclaves, at a temperature of from 120°C to 200°C for a time sufficient for crystallization to occur at the temperature used, e.g., from 1 to 15 days.
• Crystallization is usually carried out in a closed system under autogenous pressure.
• the solid product is recovered from the reaction mixture by standard mechanical separation techniques such as centrifugation or filtration.
• the crystals are water-washed and then dried to obtain the as-synthesized molecular sieve crystals.
• the drying step is typically performed at a temperature of less than 200°C.
• the recovered crystalline molecular sieve product contains within its pore structure at least a portion of the structure directing agent used in the synthesis.
• the molecular sieve described herein may be subjected to subsequent treatment to remove part or all of the structure directing agent used in its synthesis.
• This can be conveniently effected by thermal treatment in which the as-synthesized material can be heated at a temperature of at least 370°C for at least 1 minute and not longer than 24 hours.
• the thermal treatment can be performed at a temperature up to 925°C. While sub-atmospheric and/or super-atmospheric pressures can be employed for the thermal treatment, atmospheric pressure may typically be desired for reasons of convenience.
• the structure directing agent can be removed by treatment with ozone (see, e.g., A.N. Parikh et ai, Micropor.
• the original Group 1 or 2 metal cations (e.g., Na + ) in the as-synthesized molecular sieve can be replaced in accordance with techniques well known in the art by ion exchange with other cations.
• Preferred replacing cations include metal ions, hydrogen ions, hydrogen precursor (e.g., ammonium) ions and mixtures thereof.
• Particularly preferred replacing cations are those which tailor the catalytic activity for certain chemical conversion reactions. These include hydrogen, rare earth metals and metals of Groups 2 to 15 of the Periodic Table of the Elements.
• Such components can include active and inactive materials and synthetic or naturally occurring zeolites, as well as inorganic materials such as clays, silica, and/or metal oxides such as alumina.
• the latter may be either naturally occurring or in the form of gelatinous precipitates or gels including mixtures of silica and other metal oxides.
• Use of a material in conjunction with SSZ- 108 i.e., combined therewith or present during synthesis of the crystalline material, which can be in its active state) can tend to change the level of conversion and/or selectivity of the catalyst in certain chemical conversion processes.
• Inactive materials can suitably serve as diluents, e.g., to control the amount of conversion in a given process, so that products can be obtained in an economic and orderly manner, such as without employing other means for controlling the rate of reaction.
• These materials may be incorporated into naturally occurring clays (e.g., bentonite and/or kaolin) to improve the crush strength of the catalyst under commercial operating conditions.
• These materials i.e., clays, oxides, etc.
• binders for the catalyst It can be desirable to provide a catalyst having good crush strength, because, in commercial use, it can be desirable to prevent/limit the catalyst from breaking down into powder-like materials (fines).
• These clay and/or oxide binders can be employed, for example, solely to improve the crush strength of the catalyst.
• Naturally occurring clays that can be composited with SSZ-108 can include the montmorillonite and kaolin families, which families include the sub- bentonites, and the kaolins commonly known as Dixie, McNamee, Georgia and Florida clays, as well as others in which the main mineral constituent is halloysite, kaolinite, dickite, nacrite, or anauxite. Such clays can be used in the raw state (as originally mined) and/or initially subjected to calcination, acid treatment, and/or chemical modification. Binders useful for compositing with SSZ-108 can additionally or alternately include inorganic oxides, such as silica, zirconia, titania, magnesia, beryllia, alumina, and mixtures thereof.
• inorganic oxides such as silica, zirconia, titania, magnesia, beryllia, alumina, and mixtures thereof.
• SSZ- 108 can be composited with a porous matrix material, such as silica-alumina, silica- magnesia, silica-zirconia, silica-thoria, silica-beryllia, silica-titania, as well as ternary compositions such as silica-alumina-thoria, silica-alumina-zirconia, silica-alumina- magnesia, silica-magnesia-zirconia, and mixtures thereof.
• a porous matrix material such as silica-alumina, silica- magnesia, silica-zirconia, silica-thoria, silica-beryllia, silica-titania, as well as ternary compositions such as silica-alumina-thoria, silica-alumina-zirconia, silica-alumina- magnesia, silica-magnesia-zirconia
• the relative proportions of SSZ-108 and inorganic oxide matrix may vary widely, with the SSZ-108 content typically ranging from 1 to 90 wt. % (e.g., 2 to 80 wt. %), based on the total composite weight.
• the present molecular sieve has a chemical composition comprising the following molar relationship:
• compositional variables Q and M are as described herein above.
• the as-synthesized form of the present molecular sieve may have molar ratios different from the molar ratios of reactants of the reaction mixture used to prepare the as-synthesized form. This result may occur due to incomplete incorporation of 100% of the reactants of the reaction mixture into the crystals formed (from the reaction mixture).
• the present molecular sieve has a chemical composition comprising the following molar relationship:
• n has a value of from 5 to 25 (e.g., 5 to 20, or 5 to 15).
• the novel molecular sieve structure SSZ-108 is characterized by a powder X-ray diffraction pattern, which in the as-synthesized form of the molecular sieve, includes at least the lines listed in Table 2 below and which, in the calcined form of the molecular sieve, includes at least the peaks listed in Table 3 below.
• Peak broadening is characterized by the Full-Width at Half Maximum (FWH M) of the XRD peak. Based on the FWHM values, the peaks are classified as:
• the powder XRD patterns provided are based on a relative intensity scale in which the strongest line in the XRD pattern is assigned a value of 100:
• the present molecular sieve may be used as a sorbent or a catalyst for a variety of chemical reactions.
• the present molecular sieve is particularly suited for use as a catalyst for organic conversion processes and for the reduction of nitrogen oxides in a gas stream.
• organic conversion processes which may be catalyzed by the present molecular sieve include, but are not limited to, animating lower alcohols and converting organic oxygenates to one or more olefins. Such reactions may be catalyzed by contacting the respective feedstock with a catalyst comprising SSZ-108 under conditions sufficient to affect the named transformation.
• the present molecular sieve may be used in the catalytic conversion of organic oxygenates to one or more olefins, particularly ethylene and propylene.
• organic oxygenates is defined herein to include aliphatic alcohols, ethers, carbonyl compounds (e.g., aldehydes, ketones, carboxylic acids, carbonates, and the like), and also compounds containing hetero-atoms, such as, halides, mercaptans, sulfides, amines, and mixtures thereof.
• the aliphatic moiety normally contains from 1 to 10 carbon atoms (e.g., 1 to 4 carbon atoms).
• Representative organic oxygenates include lower straight chain or branched aliphatic alcohols, their unsaturated counterparts, and their nitrogen, halogen, and sulfur analogs.
• suitable organic oxygenate compounds include methanol; ethanol; n-propanol; isopropanol; C 4 to Go alcohols; methyl ethyl ether; dimethyl ether; diethyl ether; diisopropyl ether; formaldehyde; dimethyl carbonate; acetone; acetic acid; n-alkyl amines, n-alkyl halides, n-alkyl sulfides having n-alkyl groups in a range of from 3 to 10 carbon atoms; and mixtures thereof.
• oxygenate compounds are methanol, dimethyl ether, or combinations thereof, especially methanol.
• a feedstock comprising an organic oxygenate is contacted in the vapor phase in a reaction zone with a catalyst comprising the present molecular sieve at effective process conditions so as to produce the desired olefins.
• the process may be carried out in a liquid or a mixed vapor/liquid phase.
• different conversion rates and selectivities of feedstock-to-product may result depending upon the catalyst and the reaction conditions.
• the diluent is generally non-reactive to the feedstock or molecular sieve catalyst composition and is typically used to reduce the
• Non-limiting examples of suitable diluents include helium, argon, nitrogen, carbon monoxide, carbon dioxide, water, essentially non-reactive paraffins (especially alkanes such as methane, ethane, and propane), essentially non-reactive aromatic compounds, and mixtures thereof.
• the most preferred diluents are water and nitrogen, with water being particularly preferred.
• Diluent(s) may comprise from 1 to 99 mol % of the total feed mixture.
• the temperature employed in the oxygenate conversion process may vary over a wide range, such as from 200°C to 1000° C (e.g., 250°C to 800°C, 300°C to 650°C, or 400°C to 600°C).
• Light olefin products will form, although not necessarily in optimum amounts, at a wide range of pressures, including autogenous pressures and pressures in the range of from 0.1 kPa to 10 MPa (e.g., 7 kPa to 5 MPa, or 50 kPa to 1 MPa).
• the foregoing pressures are exclusive of diluent, if any is present, and refer to the partial pressure of the feedstock as it relates to oxygenate compounds and/or mixtures thereof. Lower and upper extremes of pressure may adversely affect selectivity, conversion, coking rate, and/or reaction rate; however, light olefins such as ethylene and/or propylene may still may form.
• the oxygenate conversion process should be continued for a period of time sufficient to produce the desired olefin products.
• the reaction time may vary from tenths of seconds to a number of hours.
• the reaction time is largely determined by the reaction temperature, the pressure, the catalyst selected, the weight hourly space velocity, the phase (liquid or vapor), and the selected process design characteristics.
• WHSV weight hourly space velocities
• the WHSV generally may be in the range of from 0.01 to 500 hr 1 (e.g., 0.5 to 300 hr 1 , or 1 to 200 hr 1 ).
• the present molecular sieve may be used in the selective catalytic reduction (SCR) of nitrogen oxides.
• SCR selective catalytic reduction
• a gas stream comprising nitrogen oxides ( ⁇ ) is selectively reduced in the presence of a reductant and a catalyst comprising the present molecular sieve.
• the nitrogen oxides (principally NO and N0 2 ) are reduced to N 2 while the reductant is oxidized.
• ammonia is the reductant
• N 2 is also an oxidation product.
• the only reaction products are water and N 2 , although some NH3 is usually oxidized with air to NO or N 2 0.
• one more transition metals may be incorporated into the molecular sieve support. Any suitable transition metal may be selected. Transition metals particularly effective for use during selective catalytic reduction include one or more of Cr, Mn, Fe, Co, Ce, Ni, Cu, Mo, Ru, Rh, Pd, Ag, Re, Ir, and Pt. In one embodiment, the transition metal is selected from Fe and Cu. In an exemplary embodiment, the transition metal is Cu. Any suitable and effective amount of transition metal may be used in the catalyst. The total amount of the transition metal(s) that may be included in the molecular sieve may be from 0.01 to 20 wt. % (e.g., 0.1 to 10 wt. %, 0.5 to 5 wt. %, or 1 to 2.5 wt. %) based on the total weight of the molecular sieve support.
• the total amount of the transition metal(s) that may be included in the molecular sieve may be from 0.01 to 20 wt. % (e.g., 0.1 to 10
• the molecular sieve catalyst may be used in any suitable form.
• the molecular sieve catalyst may be used in powder form, as extrudates, as pellets, or in any other suitable form.
• the molecular sieve catalyst for use in the reduction of nitrogen oxides may be coated on a suitable substrate monolith or can be formed as extruded-type catalysts, but is preferably used in a catalyst coating.
• the molecular sieve catalyst is coated on a flow-through monolith substrate (i.e., a honeycomb monolithic catalyst support structure with many small, parallel channels running axially through the entire part) or filter monolith substrate, such as a wall- flow filter, etc.
• the molecular sieve catalyst for use herein may be coated (e.g., as a washcoat component) on a suitable monolith substrate, such as a metal or ceramic flow through monolith substrate or a filtering substrate, such as a wall-flow filter or sintered metal or partial filter.
• a suitable monolith substrate such as a metal or ceramic flow through monolith substrate or a filtering substrate, such as a wall-flow filter or sintered metal or partial filter.
• the molecular sieve may be synthesized directly onto the substrate and/or may be formed into an extruded-type flow through catalyst.
• the gas stream comprising nitrogen oxides may contain one or more of NO, N0 2 , and N 2 0 in addition to other non-NO x gases such as N 2 , 0 2 , CO, C0 2 , SO2, HCI and H2O.
• the gas stream may contain from 1 to 10,000 ppm (e.g., 10 to 1,000 ppm, or 50 to 500 ppm) of NO.
• the gas stream comprising nitrogen oxides may be an exhaust gas derived from a combustion process, such as from an internal combustion engine (whether mobile or stationary), a gas turbine or coal or oil fired plants.
• the reductant can be a nitrogen compound or a short-chain (e.g., Ci to Cs) hydrocarbon.
• the reductant is a nitrogen compound.
• Suitable nitrogen compounds include ammonia, hydrazine, and ammonia precursors (e.g., urea, ammonium carbonate, ammonium carbamate, ammonium hydrogen carbonate, and ammonium formate).
• the gas stream comprising nitrogen oxides can contact the catalyst at a gas hourly space velocity of from 5000 to 500,000 hf 1 (e.g., 10,000 to 200,000 h _1 ).
• the reduction of nitrogen oxides may be carried out at a temperature within the range of 100°C to 650°C (e.g., 250°C to 600°C).
• the reduction of nitrogen oxides may be carried out in the presence of oxygen or in the absence of oxygen.
• Powder XRD of the as-synthesized product gave the pattern indicated in FIG. 1 and showed the product to be a pure form of a new phase, designated SSZ- 108.
• a SEM image of the as-synthesized product is shown in FIG. 2 indicating a uniform field of crystals.
• the as-synthesized product had a S1O2/AI2O3 molar ratio of 8.82, as determined by ICP elemental analysis.
• Powder XRD showed the product to be pure SSZ-108.
• the as-synthesized product had a S1O2/AI2O3 molar ratio of 8.24, as determined by ICP elemental analysis.
• Powder XRD showed the product to be a mixture of SSZ-108 and ANA framework type zeolite.
• Powder XRD showed the product to be pure SSZ-108.
• Powder XRD showed the product to be a mixture of SSZ-108 and ANA framework type zeolite.
• Powder XRD of the calcined product gave the pattern indicated in FIG. 3 and showed the material to be stable after calcination to remove the organic structure directing agent.
• the product (NH 4 -SSZ-108) was subjected to micropore volume analysis using N 2 an adsorbate and via the B.E.T. method.
• the molecular sieve had a micropore volume of 0.15 cm 3 /g.

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